CN2611016Y - Novel adsorption tower with built-in heat-exchanger - Google Patents
Novel adsorption tower with built-in heat-exchanger Download PDFInfo
- Publication number
- CN2611016Y CN2611016Y CN 03230582 CN03230582U CN2611016Y CN 2611016 Y CN2611016 Y CN 2611016Y CN 03230582 CN03230582 CN 03230582 CN 03230582 U CN03230582 U CN 03230582U CN 2611016 Y CN2611016 Y CN 2611016Y
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- Prior art keywords
- heat exchanger
- built
- model
- utility
- adsorption tower
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- Separation Of Gases By Adsorption (AREA)
Abstract
The utility model discloses a novel adsorption column with a build-in heat exchanger including a casing and a support, characterized in that a heat exchanger is provided in the box. The utility model has the advantages of rational structure, skillful concept. The utility model not only keeps absorbing in suitable temperature, but also shortens cooling time after reactivation and reduces cooling gas amount greatly thereby reducing operating cost greatly and worth spreading out.
Description
Technical field:
The utility model relate to a kind of handle and process for purifying gas, tail gas, waste gas technical process in equipment, belong to chemical industry, environmental protection equipment technical field.
Background technology:
At present, the adsorption plant in other devices exists: 1. be hard to keep and adsorb under suitable temperature, 2. the regeneration back is longer cool time, 3. the defectives such as large usage quantity of cold gas.
Summary of the invention:
Technical problem to be solved in the utility model provides and a kind ofly can effectively overcome above-mentioned defective, reduces the novel adsorption tower of the built-in heat exchanger of operating cost.The technical scheme that its technical problem that solves the utility model adopts is, a kind of novel adsorption tower of built-in heat exchanger mainly is made up of casing and bearing etc., and its characteristics are: be provided with heat exchanger in the casing.Owing to adopt such scheme, be not difficult to draw and the utlity model has following beneficial effect, the utility model is rational in infrastructure, be skillfully constructed, both can remain under the suitable temperature and adsorb, shorten the time of regeneration back cooling again, reduce the consumption of cold gas widely, thereby greatly reduced operating cost, the tool promotional value.
Description of drawings:
Below in conjunction with drawings and Examples the utility model is described in further detail.
Fig. 1 is a structural representation of the present utility model.
The specific embodiment:
Among the figure, the profile of this equipment box 80 is cylinders (also cube) of a tower shape, the bottom of casing 80 is a bearing 50, upper cover 60 is provided with material inlet 30, low head 70 is provided with material outlet 40, alternately be equipped with monolayer adsorption bed 20 and heat exchanger 10 in the casing 80, adsorption bed 20 mainly contains formations such as adsorbent, silk screen 21, Ge Gate 22, securing member, adsorbent is from the charging of adsorbent and tear material mouthfuls 23,24 open and install and remove, and adsorbent can be active carbon, molecular sieve, silicic acid, resin etc.The height of each layer bed can be the same or different, mainly decide by process requirement of equipment, heat exchanger 10 is provided with the import and export 11,12 of cooling agent or heating agent, the pattern of heat exchanger 10 can adopt coiled, also available column tubular type, board-like, calandria, winding tubular type or the like, the heat transfer area of each heat exchanger is at 0.5m
2-1000m
2Between, adopt suitable heat transfer area according to different technological requirements, so each heat exchanger area can equate also can be unequal, heat exchanger tube in the heat exchanger can adopt light pipe, can also adopt finned tube, helix tube etc., the heat exchanger cooling medium can be selected cooling water, chilled brine or other cooling things for use according to different process.
Claims (3)
1, a kind of novel adsorption tower of built-in heat exchanger mainly is made up of casing and bearing etc., it is characterized in that: be provided with heat exchanger in the casing.
2, by the novel adsorption tower of the described a kind of built-in heat exchanger of claim 1, it is characterized in that: described adsorption bed is made up of adsorbent, silk screen, Ge Gate etc.
3, by the novel adsorption tower of claim 1 or 2 described a kind of built-in heat exchangers, it is characterized in that: described adsorption bed is divided into two-layer at least, and heat exchanger is located between two adsorption bed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03230582 CN2611016Y (en) | 2003-04-22 | 2003-04-22 | Novel adsorption tower with built-in heat-exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03230582 CN2611016Y (en) | 2003-04-22 | 2003-04-22 | Novel adsorption tower with built-in heat-exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2611016Y true CN2611016Y (en) | 2004-04-14 |
Family
ID=34165334
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 03230582 Expired - Lifetime CN2611016Y (en) | 2003-04-22 | 2003-04-22 | Novel adsorption tower with built-in heat-exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2611016Y (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102188888A (en) * | 2011-04-12 | 2011-09-21 | 王晓晔 | A wet method treatment process of purified flue gas with a water collection function in the process and a processing apparatus thereof |
| CN102335541A (en) * | 2011-08-24 | 2012-02-01 | 中国寰球工程公司 | Absorption tower |
| CN101721833B (en) * | 2008-10-28 | 2012-02-29 | 中国石油化工股份有限公司 | Method for recovering and purifying hydrocarbon wastegas by condensation and adsorption |
| CN102941001A (en) * | 2012-11-02 | 2013-02-27 | 江苏航天惠利特环保科技有限公司 | Adsorption plant |
| CN103193923A (en) * | 2012-01-10 | 2013-07-10 | 苏州国家环保高新技术产业园发展有限公司 | Preparation method and application of pervaporation separation material based on polyacrylate resin |
| CN110711459A (en) * | 2019-10-28 | 2020-01-21 | 海湾环境科技（北京）股份有限公司 | Oil gas recovery system |
| WO2023125173A1 (en) * | 2021-12-30 | 2023-07-06 | 西安蓝晓科技新材料股份有限公司 | Resin column device |
-
2003
- 2003-04-22 CN CN 03230582 patent/CN2611016Y/en not_active Expired - Lifetime
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101721833B (en) * | 2008-10-28 | 2012-02-29 | 中国石油化工股份有限公司 | Method for recovering and purifying hydrocarbon wastegas by condensation and adsorption |
| CN102188888A (en) * | 2011-04-12 | 2011-09-21 | 王晓晔 | A wet method treatment process of purified flue gas with a water collection function in the process and a processing apparatus thereof |
| CN102335541A (en) * | 2011-08-24 | 2012-02-01 | 中国寰球工程公司 | Absorption tower |
| CN102335541B (en) * | 2011-08-24 | 2013-08-07 | 中国寰球工程公司 | Absorption tower |
| CN103193923A (en) * | 2012-01-10 | 2013-07-10 | 苏州国家环保高新技术产业园发展有限公司 | Preparation method and application of pervaporation separation material based on polyacrylate resin |
| CN103193923B (en) * | 2012-01-10 | 2015-05-27 | 苏州国家环保高新技术产业园发展有限公司 | Preparation method and application of pervaporation separation material based on polyacrylate resin |
| CN102941001A (en) * | 2012-11-02 | 2013-02-27 | 江苏航天惠利特环保科技有限公司 | Adsorption plant |
| CN110711459A (en) * | 2019-10-28 | 2020-01-21 | 海湾环境科技（北京）股份有限公司 | Oil gas recovery system |
| WO2023125173A1 (en) * | 2021-12-30 | 2023-07-06 | 西安蓝晓科技新材料股份有限公司 | Resin column device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: SHANGHAI ZORAN ENGINEERING CO., LTD. Free format text: FORMER NAME OR ADDRESS: ZHUORAN ENVIRONMENTAL ENGINEERING CO., LTD., SHANGHAI |
|
| CP01 | Change in the name or title of a patent holder |
Patentee after: Shanghai?Zuoran?Engineering?Technology?Co., Ltd. Patentee before: Zhuoran Environment Engineering Co., Ltd., Shanghai |
|
| ASS | Succession or assignment of patent right |
Owner name: SHANGHAI XITAI ENGINEERING DESIGN CO., LTD Free format text: FORMER OWNER: SHANGHAI ZHUORAN ENGINEERING TECHNOLOGY CO.,LTD. Effective date: 20090417 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20090417 Address after: Room 689, No. 1604, Guangdong Road, Shanghai, 200001 Patentee after: Shanghai Xitai Engineering Design Co. Ltd. Address before: Room 689, No. 1603, Guangdong Road, Shanghai, 200001 Patentee before: Shanghai?Zuoran?Engineering?Technology?Co., Ltd. |
|
| C56 | Change in the name or address of the patentee |
Owner name: ZHUORAN ENGINEERING TECH CO., LTD., SHANGHAI Free format text: FORMER NAME: SHANGHAI XITAI ENGINEERING DESIGN CO., LTD. |
|
| CP03 | Change of name, title or address |
Address after: 200001 Shanghai City, Huangpu District Guangdong Road No. 689 room 1603 Patentee after: Shanghai?Zuoran?Engineering?Technology?Co., Ltd. Address before: 1604 room 689, 200001 Guangdong Road, Shanghai Patentee before: Shanghai Xitai Engineering Design Co. Ltd. |
|
| C56 | Change in the name or address of the patentee | ||
| CP02 | Change in the address of a patent holder |
Address after: 200335 Shanghai city Changning District road 268 Lane 3, facing the new Patentee after: Shanghai?Zuoran?Engineering?Technology?Co., Ltd. Address before: 200001 Shanghai City, Huangpu District Guangdong Road No. 689 room 1603 Patentee before: Shanghai?Zuoran?Engineering?Technology?Co., Ltd. |
|
| C17 | Cessation of patent right | ||
| CX01 | Expiry of patent term |
Expiration termination date: 20130422 Granted publication date: 20040414 |